Refining Apparatus and Refining Method for Recycling Waste Plastics

ABSTRACT

A refining apparatus and a refining method for recycling waste plastics. The refining apparatus includes a feeding device, a pyrolysis furnace, a chloride-decomposing device, a first condensation device, a temporary storage, a still, a sieve plate tower, a second condensation device, and a receiving tank. The waste plastics are cracked by the pyrolysis furnace to produce plastic gas by heating. The chlorides of the plastic gas are removed by the chloride-decomposing device having the ammonia to produce a first oil gas. The first oil gas is condensed by the first condensation device to produce raw oil. The raw oil is heated by the still to produce a second oil gas. The second oil gas is sieved by the sieve plate tower to produce a third oil gas. The third oil gas is condensed by the second condensation device to produce finished oil received by the receiving tank.

CROSS-REFERENCE TO RELATED APPLICATION

This application is a divisional of U.S. patent application Ser. No.14/325481, filed on Jul. 8, 2014, which claims the benefit of TaiwanIntellectual Property Office Application No. 103108975, filed on Mar.13, 2014, in the Taiwanese Intellectual Property Office, the disclosuresof which are incorporated herein their entirety by reference.

BACKGROUND OF THE INVENTION

1. Field of the Invention

The present invention relates to an apparatus and method for recyclingwaste plastics, in particular with respect to a refining apparatus and arefining method for recycling waste plastics.

2. Description of the Related Art

With the development of technology and progress of civilization, peoplereply more and more on products of petrochemical industry, such asplastic product and gasoline and so on. However, as the amount of thepetroleum crude oil used in the petrochemical industry has beendeclining as people's excessive dependence; recently, countries over theworld have been developing the economy while engaging in how to reducethe usage of the petroleum crude oil.

In addition, people also have to process the waste plastics generated bythe used plastic products, and if the waste plastics are buried, theplastic, which is difficult to decompose is not easy to decay, and italso destroys the soil environment. Consequently, the waste landfillwill inevitably cause severe environmental problem. With the gradualincrease of environmental protection consciousness, countries over theworld will dedicate to the development of environmental industry andsubstantially commercialize the application to the environmentalprocess. However, the problem is that the current technology stillcannot refine the recycling waste plastics as the renewable oil of highpurity by using the limited resource effectively.

SUMMARY OF THE INVENTION

In view of the aforementioned defects, the purpose of the presentinvention is to provide a refining apparatus and a refining method forrecycling waste plastics to refine the waste plastics as the renewableoil having high purity by using the limited resource effectively.

In order to achieve the preceding purpose, the present invention mayprovide a refining apparatus for recycling waste plastics at leastcomprising: a feeding device providing waste plastics; a pyrolysisfurnace having a rotary kiln and a burner, the rotary kiln connectedwith the feeding device for receiving the waste plastics and beingrotating, the burner being assembled under the rotary kiln and burning afuel for providing heat to the waste plastics in the rotary kiln, so asto crack the waste plastics to produce a plastic gas; achloride-decomposing device having ammonia and being assembled above therotary kiln, wherein chlorine of the plastic gas are removed and a firstoil gas and a mixed gas are produced by reacting the plastic gas withthe ammonia in the chloride-decomposing device; a first condensationdevice connecting with the chloride-decomposing device for enabling thefirst oil gas and the mixed gas floating into the first condensationdevice, wherein the first condensation device condenses the first oilgas to produce a raw oil; a temporary storage being assembled under thefirst condensation device and receiving the raw oil; a still receivingthe raw oil from the temporary storage and heating the raw oil toproduce a second oil gas; a sieve plate tower connected above the stillfor enabling the second oil gas floating upwardly in the sieve platetower, and having a plurality of sieve plates arranged in a verticaldirection orderly sieving the second oil gas, respectively; wherein aheavier oil gas of the second oil gas is transformed into an oil via thesieve plates and sent back to the still, and a lighter oil gas of thesecond oil gas floats through the sieve plates to produce a third oilgas; a second condensation device connecting with the sieve plate towerand condensing the third oil gas to produce a finished oil; and areceiving tank being assembled under the second condensation device andreceiving the finished oil.

Wherein, the refining apparatus for recycling waste plastics of thepresent invention may further comprise: a tundish assembled between thefeeding device and the pyrolysis furnace; a bunker elevator connectingthe feeding device and the tundish, and carrying the waste plastics fromthe feeding device to the tundish; and a screw extruder connecting thetundish and the rotary kiln, and extruding the waste plastics from thetundish to the rotary kiln.

Wherein, the refining apparatus for recycling waste plastics of thepresent invention may further comprise a pipe connecting the firstcondensation device and the burner, the mixed gas floating from thefirst condensation device to the burner via the pipe for serving as thefuel, thereby the intermediate product of the refining process, such asthe mixed gas, can be used effectively.

Wherein, the refining apparatus for recycling waste plastics of thepresent invention may further comprise a vacuum device connected betweenthe first condensation device and the temporary storage and beingadjacent to the temporary storage, wherein the vacuum device has afiltering tank and a vacuum tank connecting with each other, wherein thevacuum tank accelerates the raw oil flowing to the temporary storage andthe filtering tank blocks the raw oil and an impurity from flowing intothe vacuum tank.

Wherein, the refining apparatus for recycling waste plastics of thepresent invention may further comprise a preheating device beingassembled between the sieve plate tower and the second condensationdevice, wherein the preheating device has two pipes designed to exchangeheat, wherein one pipe of the two pipes connects with the sieve platetower to carry the third oil gas and cool down the third oil gas viaheat exchange, and the other pipe connects with the temporary storageand the still to carry the raw oil from the temporary storage to thestill and thereby to warm up the raw oil via the heat exchange.

In addition, the present invention may further provide a refining methodfor recycling waste plastics, at least comprising following steps:providing waste plastics in a feeding device; carrying the wasteplastics to a rotary kiln of a pyrolysis furnace, wherein the rotarykiln rotates the waste plastics; providing heat to the waste plastics inthe rotary kiln by burning a fuel via a burner, so that the wasteplastics being cracked to produce a plastic gas, wherein the burner isassembled under the rotary kiln; introducing the plastic gas into achloride-decomposing device having ammonia to remove chlorine of theplastic gas and produce a first oil gas and a mixed gas by reacting thewaste plastics with the ammonia; condensing the first oil gas to producea raw oil by a first condensation device; receiving the raw oil by atemporary storage; receiving the raw oil from the temporary storage by astill, wherein the still warms up the raw oil to produce a second oilgas; introducing the second oil gas into a sieve plate tower, whereinthe sieve plate tower has a plurality of sieve plates arranged in avertical direction orderly to sieve the second oil gas, respectively,wherein a heavier oil gas of the second oil gas is transformed into anoil via the sieve plates and sent back to the still, and a lighter oilgas of the second oil gas floats through the sieve plates to produce athird oil gas; condensing the third oil gas to produce a finished oil bya second condensation device; and receiving the finished oil by areceiving tank.

Wherein, the step of carrying the waste plastics to a rotary kiln of apyrolysis furnace may comprise the following steps: carrying the wasteplastics from the feeding device to a tundish by a bunker elevator; andextruding the waste plastics from the tundish to the rotary kiln by ascrew extruder.

Wherein, the mixed gas may be carried to the burner for serving as thefuel by a pipe when the mixed gas is produced.

Wherein, the refining method for recycling waste plastics of the presentinvention may further comprise the following step: using a filteringtank and a vacuum tank to accelerate the raw oil flowing to thetemporary storage.

Wherein, the refining method for recycling waste plastics of the presentinvention may further comprise the following step: exchanging heatbetween the third oil gas and the raw oil by a preheating device to cooldown the third oil gas and warm up the raw oil gas carried from thetemporary storage to the still when the third oil gas is produced.

As a result, according to a refining apparatus and a refining method forrecycling waste plastics of the present invention, there are one or moreadvantages as follows:

(1) The burner uniformly provides heat to the waste plastics in therotary kiln by rotating the rotary kiln.

(2) The sieve plate tower respectively sieves the second oil gas, sothat the lighter oil gas floats through the sieve plates to produce athird oil gas, so as to refine the recycling waste plastics as therenewable oil having higher purity by using the limited resourceeffectively.

(3) A screw extruder orderly extrudes the waste plastics from thetundish to the rotary kiln so as to control the amount of the wasteplastics in the rotary kiln.

(4) A preheating device transfers the heat of the third oil gas to theraw oil so as to reduce the amount of fuel.

BRIEF DESCRIPTION OF THE DRAWINGS

FIG. 1 is a schematic diagram of the first embodiment of a raw oilobtaining device of a refining apparatus for recycling waste plasticsaccording to the present invention.

FIG. 2 is a schematic diagram of the second embodiment of a raw oilobtaining device of a refining apparatus for recycling waste plasticsaccording to the present invention.

FIG. 3 is a schematic diagram of the first embodiment of a rear enddevice of a refining apparatus for recycling waste plastics according tothe present invention.

FIG. 4 is a schematic diagram of the second embodiment of a rear enddevice of a refining apparatus for recycling waste plastics according tothe present invention.

FIG. 5 is a flow chart of a refining method for recycling waste plasticsaccording to the present invention.

DETAILED DESCRIPTION OF THE PREFERRED EMBODIMENTS

Please with reference to FIG. 1 and FIG. 3, FIG. 1 is a schematicdiagram of the first embodiment of a raw oil obtaining device of arefining apparatus for recycling waste plastics according to the presentinvention, and FIG. 3 is a schematic diagram of the first embodiment ofa rear end device of a refining apparatus for recycling waste plasticsaccording to the present invention. As FIG. 1 and FIG. 3 show, arefining apparatus for recycling waste plastics of the present inventioncomprises a raw oil obtaining device 102 refining the waste plastics asraw oil and a rear end device 201 further refining the raw oil asfinished oil. Wherein, the raw oil obtaining device 102 at leastcomprises a feeding device 111, a pyrolysis furnace 115, achloride-decomposing device 130, a first condensation device 140 and atemporary storage 160; and the rear end device 201 at least comprises astill 210, a sieve plate tower 220, a second condensation device 232 anda receiving tank 240.

Wherein, the feeding device 111 is used to provide waste plastics. Forexample, the feeding device 111 can be a concave tank comprising anaccommodating space, so a user can place the waste plastics in theaccommodating space of the concave tank, wherein the waste plastics canbe Polypropylene (PP) plastic, Polyethylene (PE) plastic or Polystyrene(PS) plastic. When the feeding device 111 is fed with the wasteplastics, the pyrolysis furnace 115 connected with the feeding device111 receives the waste plastics from the feeding device 111. Besides,the rotary kiln of the pyrolysis furnace 115 is rotated to rotate thewaste plastics, which are received. Please with reference to FIG. 2, itis a schematic diagram of the second embodiment of a raw oil obtainingdevice of a refining apparatus for recycling waste plastics according tothe present invention. As shown in FIG. 1 to FIG. 3, the differencesbetween the raw oil obtaining device 101 of the second embodiment andthe raw oil obtaining device 102 of the first embodiment are that theraw oil obtaining device 101 of the second embodiment further has abunker elevator 112, a tundish 113 and a screw extruder 114 between thefeeding device 111 and the pyrolysis furnace 115 so as to carry thewaste plastics from the feeding device 111 to the pyrolysis furnace 115,and the pyrolysis furnace 115 further comprises a burner 120.

Moreover, the tundish 113 of the raw oil obtaining device 101 isdisposed between the feeding device 111 and the pyrolysis furnace 115,the bunker elevator 112 connects the feeding device 111 and the tundish113, and the bunker elevator 112 can be a conveyor belt with an inclinedangle, so that the bunker elevator 112 can convey the waste plasticsfrom the feeding device 111 to the tundish 113. The screw extruder 114connects the tundish 113 and the rotary kiln of the pyrolysis furnace115. For example, the screw extruder 114 is assembled under the tundish113 to receive the waste plastics and extrudes the waste plasticsreceived from the tundish 113 to the rotary kiln. When the pyrolysisfurnace 115 receives the waste plastics, the rotary kiln conductsrotating to rotate the waste plastics. Besides, the pyrolysis furnace115 further has the burner 120 which is assembled under the rotary kiln.Wherein, the burner 120 burns a fuel for providing heat to the wasteplastics in the rotary kiln, so as to crack the waste plastics toproduce a plastic gas. Wherein, the fuel, which the burner 120 uses, canbe any flammable objects or gases.

Besides, the pyrolysis furnace 115 can be a metal material cylinderwhich can electromagnetically heat the waste plastics in the pyrolysisfurnace 115 and irradiate with microwave to the heated waste plastics soas to crack the waste plastics to produce the plastic gas through ashorter duration and limited energy resource. For example, the pyrolysisfurnace 115 can have a frequency conversion electromagnetic heater (notshown) which transforms electrical energy into heat energy viaelectromagnetic induction. For instance, the alternating current of 220V or 380 V and 60 Hz is transformed into a high frequency voltage of20-40 KHz, and the current of the high frequency voltage flows through acoil to produce an alternating magnetic field of high-speedtransformation, so that the conductive metal material produces a numberof vortexes in the metal for enabling the metal material cylinderpromptly heating itself and thereby warming up the waste plastics. Then,microwave is irradiated to the waste plastics, which are warmed up bythe electromagnetic heater. The microwave energy can be absorbed by thewaste plastics according to the interaction of the waste plastics andthe microwave to reduce the activating energy among the particles of thewaste plastics. So, the micro-densification speed of the waste plasticscan be accelerated to quicken the sinter of the waste plastics forproducing the plastic gas.

The chloride-decomposing device 130 having ammonia is assembled abovethe rotary kiln of the pyrolysis furnace 115. For example, thechloride-decomposing device 130 can be an ammonia cylinder assembledabove the rotary kiln, when the pyrolysis furnace 115 produces theplastic gas, the plastic gas will be reacted with the ammonia in thechloride-decomposing device 130 to remove the chlorides, which iscontained in the plastic gas, and produce the first oil gas and themixed gas without chlorides. Wherein, the mixed gas can be hydrogen,nitrogen and non-condensing gas and the non-condensing gas can bemethane, ethane, propane or butane. Furthermore, a gas channel isfurther assembled between the chloride-decomposing device 130 and thepyrolysis furnace 115, such that the plastic gas floats into thechloride-decomposing device 130 along the gas channel.

A first condensation device 140 is connected with thechloride-decomposing device 130 via pipe 181 for enabling the first oilgas, which is produced by the chloride-decomposing device 130, floatinginto the first condensation device 140 along the pipe 181. Wherein, thefirst oil gas is condensed by the first condensation device 140 toproduce raw oil. For example, the first condensation device 140 can be ashell and tube condenser having water tubes, when the first oil gas andthe mixed gas floats into the first condensation device 140 and contactto the water tubes, the first oil gas is condensed as fluid to producethe raw oil because the first oil gas has the higher condensation point(boiling point). Besides, because the condensation point (boiling point)of the mixed gas is lower, the mixed gas will not be condensed as fluideven contacts to the water tubes. Moreover, the temporary storage 160 isassembled under the first condensation device 140, so that the raw oilproduced by the first condensation device 140 flows into the temporarystorage 160 along a channel (not shown), i.e. the temporary storage 160is used to receive the raw oil. Wherein, the temporary storage 160 canbe lying type.

In addition, the raw oil obtaining device 101 and/or 102 of the refiningapparatus for recycling waste plastics of the present invention canfurther comprises a vacuum device. The vacuum device is connectedbetween the first condensation device 140 and the temporary storage 160and is adjacent to the temporary storage 160 so as to accelerate the rawoil flowing to the temporary storage 160. For example, the vacuum devicehas a vacuum tank 171 and a filtering tank 172, wherein the filteringtank 172 is connected with the vacuum tank 171 and is adjacent to thechannel of the temporary storage 160, and the vacuum tank 171 is used tocreate a vacuum state for the channel to accelerate the raw oil flowingto the temporary storage 160. Moreover, the filtering tank 172 blocksthe raw oil and an impurity from flowing into the vacuum tank 171 as thehigh-speed flow velocity.

In addition, the raw oil obtaining device 101 and/or 102 of the refiningapparatus for recycling waste plastics of the present invention canfurther comprises the pipe 182 connecting to the first condensationdevice 140 and the burner 120, so that the mixed gas, which is remainedin gaseous state after being processed by the first condensation device140, can float from the first condensation device 140 into the burner120 through the pipe 182 for serving as fuel of the burner 120. Forexample, the pipe 182 is connected with the upper end of the firstcondensation device 140 and because the gaseous mixed gas ischaracterized of floating upwardly, the mixed gas can enter the pipe 182and float into the burner 120 along the pipe 182. Consequently, otherthan burning additional flammable objects or gases, the burner 120 alsoburns the mixed gas produced in the refining process by the refiningapparatus for recycling waste plastics of the present invention.Therefore, the refining apparatus for recycling waste plastics of thepresent invention can reduce the amount of the additional flammableobjects or gases.

Besides, the raw oil obtaining device 101 and/or 102 of the refiningapparatus for recycling waste plastics of the present invention furthercomprises sulfur removing washing tower 151, a wet type washing tower152 and a waste gas exhausting apparatus 153. Wherein, the waste gasexhausting apparatus 153 is a waste gas exhausting pipe which isconnected to the burner 120 of the pyrolysis furnace 115, so that thewaste gas produced by the fuel burned by the burner 120 can be exhaustedvia the waste gas exhausting apparatus 153. The sulfur removing washingtower 151 is assembled in a location of the waste gas exhaustingapparatus 153 and sprays lime water to the waste gas exhaustingapparatus 153, such that when the waste gas floats through the locationwhere the sulfur removing washing tower 151 sprays lime water, the wastegas reacts with the lime water to remove the sulfur contained in thewaste gas. The wet type washing tower 152 is also assembled in alocation of the waste gas exhausting apparatus 153 and compared with thesulfur removing washing tower 151, the wet type washing tower 152 can beassembled farther from the burner 120. Wherein, the wet type washingtower 152 can be disposed with two spray holes to spray water to thewaste gas exhausting apparatus 153, respectively; wherein when the wastegas contacts to the water sprayed by one of the spray holes, thetemperature of the waste gas can therefore be reduced; and when thewaste gas contacts to the water sprayed by the other spray hole, thedust in the waste gas is condensed into solid and falls, the impurity ofthe waste gas can therefore be decreased, so that the waste gasexhausted by the waste gas exhausting apparatus 153 matches up thestandard of environmental protection regulations.

Please with reference to FIG. 3 and FIG. 4 altogether, FIG. 4 is aschematic diagram of the second embodiment of a rear end device of arefining apparatus for recycling waste plastics according to the presentinvention. Wherein, the difference between the rear end device 201 ofthe first embodiment and the rear end device 200 of the secondembodiment depends on that a preheating device 231 and the temporarystorage 233 are further included between a second condensation device232 and the sieve plate tower 220 of the rear end device 201 of thefirst embodiment, and the second condensation device 232 can be a platetype condenser. The second condensation device 230 of the secondembodiment can be a shell and tube condenser, and the rear end device200 of the second embodiment can further have the vacuum tank 251 and252.

As FIG. 1 to FIG. 4 show, when the refining apparatus for recyclingwaste plastics of the present invention obtains the raw oil, the raw oilis introduced in the rear end device 201 and/or 200 to refine a finishedoil of high purity. Wherein, the still 210 of the rear end device 201 ofthe refining apparatus for recycling waste plastics receives the raw oilfrom the temporary storage 160. For example, the rear end device 201 ofthe refining apparatus for recycling waste plastics of the presentinvention further comprises the pipe 261, the preheating device 231 andthe pipe 262, wherein the preheating device 231 comprises two pipesdesigned to exchange heat, wherein one pipe of the two pipes isconnected between the pipe 261 and the pipe 262, so that the raw oilfrom the temporary storage 160 can be carried orderly along the pipe261, one pipe of the preheating device 231 and the pipe 262 to the still210 (as shown in FIG. 3). Additionally, an oil inlet 260 is alsoassembled on the still 210, so that the raw oil flows into the still 210via the oil inlet 260 (as shown in FIG. 4). Besides, the received rawoil can be warmed up by the still 210 for producing the second oil gas.

Moreover, the sieve plat tower 220 is connected above the still 210 forenabling the second oil gas floating upwardly in the sieve plate tower220. Wherein, the sieve plate tower 220 has a plurality of sieve platesarranged in a vertical direction orderly, so the second oil gas can berespectively sieved by the sieve plates when floating through the sieveplates orderly. For example, the alignment of the plurality of sieveplates in the sieve plate tower 220 is vertical to the still 210, i.e.is parallel to the floating direction of the second oil gas, such thatthe second oil gas can floats through each sieve plates, orderly.Wherein, the sieve plates are detachably assembled in the sieve platetower 220 to benefit the user by taking out or replacing the sieveplates. When the second oil gas floats through each plates orderly, aheavier oil gas of the second oil gas is transformed into the oil viathe sieve plates, and the oil is sent back to the still 210 along achannel (not shown); and a lighter oil gas of the second oil gas cantherefore float through the sieve plates to produce a third oil gas.

The second condensation device 230 is directly connected to the sieveplate tower 220 or via the pipe to condense the third oil gas to producefinished oil. Additionally, the preheating device 231 and the temporarystorage 233 can be assembled between the second condensation device 230and the sieve plate tower 220, so that the third oil gas can floatthrough the other pipe of the preheating device 231 to the temporarystorage 233. Wherein, as the two pipes of the preheating device 231conducts heat exchange, the heat of the third oil gas is carried to theraw oil to cool down the third oil gas and warm up the raw oil flowingto the still 210. Then, the third oil gas from the temporary storage 233floats into the second condensation device 232, such that the third oilgas is condensed by the second condensation device 232 so as to producethe finished oil. In addition, the receiving tank 240 is assembled underthe second condensation device 232 and receives the finished oilproduced by the second condensation device 232. Wherein, the ingredientof the finished oil can be mixed or single liquor with high purity, suchas Polyethylene, Polypropylene and/or Polystyrene with high purity.

In addition, the rear end device of the refining apparatus for recyclingwaste plastics of the present invention further comprises the vacuumtank 251 and/or 252. Wherein, the vacuum tank 251 is assembled at oneend of the still 210 to accelerate the raw oil flowing from thetemporary storage 160 to the still 210. The vacuum tank 252 is assembledon a top end of the sieve plate tower 220 or a location where isadjacent to the top end to accelerate the second oil gas floatingupwardly in the sieve plate tower 220.

As a result, the refining apparatus for recycling waste plastics of thepresent invention uses the raw oil obtaining device and the rear enddevice to achieve the purpose of refining the waste plastics as therenewable oil with high purity and reduce the consumption of the fuelresource.

Besides, the present invention further provides a refining method forrecycling waste plastics to refine the waste plastics as the renewableoil with high purity. Please with reference to FIG. 5, it is a flowchart of a refining method for recycling waste plastics according to thepresent invention. As FIG. 1 to FIG. 5 show, the refining method forrecycling waste plastics of the present invention provides the wasteplastics (step 910). For example, the refining method for recyclingwaste plastics of the present invention provides the waste plastics intothe feeding device 111 and carries the waste plastics from the feedingdevice 111 to the tundish 113 by the bunker elevator 112, and extrudesthe waste plastics from the tundish 113 to the rotary kiln of thepyrolysis furnace 115 by the screw extruder 114. Wherein, the wasteplastics can be Polypropylene (PP) plastic, Polyethylene (PE) plastic orPolystyrene (PS) plastic.

And then, the refining method for recycling waste plastics of thepresent invention cracks the waste plastics to produce the plastic gas(step 920). For example, the refining method for recycling wasteplastics of the present invention rotates the rotary kiln of thepyrolysis furnace 115 to rotate the waste plastics therein and providesheat to the waste plastics in the rotary kiln by burning the fuel viathe burner 120 to crack the waste plastics and thereby produce theplastic gas. Wherein, the burner 120 is assembled under the rotary kiln.Besides, in the step 920, it can electromagnetically heat the wasteplastics inside the pyrolysis furnace 115 and then irradiate withmicrowave to the heated waste plastics to crack the waste plastics so asto produce the plastic gas by a shorter duration and limited resource.Besides this, the refining method for recycling waste plastics of thepresent invention further assembles the sulfur removing washing tower151 and the wet type washing tower 152 on the waste gas exhaustingapparatus 153, which exhausts the waste gas produced by the burner 120.Wherein, the sulfur removing washing tower 151 and the wet type washingtower 152 individually sprays lime water and water to the waste gasexhausting apparatus 153 so as to respectively remove the sulfurcontained in the waste gas, and reduce the waste gas temperature andremove the dust of the waste gas.

And then, the refining method for recycling waste plastics of thepresent invention chloride-decomposes the waste gas to produce the mixedgas and the first oil gas (step 930). For example, the refining methodfor recycling waste plastics of the present invention assembles thechloride-decomposing device 130 having ammonia above the rotary kiln andintroduces the plastic gas into the chloride-decomposing device 130 forenabling the plastic gas reacting with the ammonia in thechloride-decomposing device 130 to remove the chlorine of the plasticgas and produce the first oil gas and the mixed gas. Wherein, the mixedgas can be hydrogen, nitrogen and non-condensing gas. The non-condensinggas can be methane, ethane, propane or butane. Then, the refining methodfor recycling waste plastics of the present invention condenses thefirst oil gas to produce the raw oil gas by the first condensationdevice 140 (step 940). For example, the refining method for recyclingwaste plastics of the present invention carries the first oil gas to thefirst condensation device 140 by the pipe 181 and condenses the firstoil gas to produce the raw oil by the first condensation device 160. Theraw oil can be received by the temporary storage 160. Wherein, the mixedgas, which is not condensed to the liquids, can be carried to the burner120 via the pipe 182 for serving as the fuel. Additionally, the refiningmethod for recycling waste plastics of the present invention furtherassembles the vacuum device having the vacuum tank 171 and the filteringtank 172 to accelerate the raw oil flowing to the temporary storage 160.

And then, the refining method for recycling waste plastics of thepresent invention heats the raw oil to produce the second oil gas (step950). For example, the refining method for recycling waste plastics ofthe present invention receives the raw oil from the temporary storage160 by the still 210. The still 210 heats the raw oil therein to producethe second oil gas. Afterward the refining method for recycling wasteplastics of the present invention sieves the second oil gas to producethe third oil gas (step 960). For example, the refining method forrecycling waste plastics of the present invention introduces the secondoil gas into the sieve plate tower 220, which has a plurality of sieveplates arranged in a vertical direction orderly to sieve the second oilgas, respectively. Wherein, the heavier oil gas of the second oil gas istransformed into an oil via the sieve plates and sent back to the still210; the lighter oil gas of the second oil gas floats through the sieveplates to produce a third oil gas. In addition, the refining method forrecycling waste plastics of the present invention can further assemblethe vacuum tank 252 on a top end of the sieve plate tower 220 or alocation where is adjacent to the top end to accelerate the second oilgas floating upwardly in the sieve plate tower 220.

And then, the refining method for recycling waste plastics of thepresent invention condenses the third oil gas to produce the finishedoil (step 970). For example, the refining method for recycling wasteplastics of the present invention directly or via the pipe enables thethird oil gas floating into the second condensation device 230, such asa shell and tube condenser, to condense the third oil gas for producingthe finished oil by the second condensation device 230. Moreover, therefining method for recycling waste plastics of the present inventionassembles the preheating device 231 between the second condensationdevice 232 and the sieve plate tower 220, such that the third oil gasfloats through one pipe of the two pipes of the preheating device 231while the raw oil carried from the temporary storage 160 to the still210 also flows through the other pipe of the preheating device 231. Suchthat the heat between the third oil gas and the raw oil can be exchangedin the preheating device 231 and thereby the third oil gas can be cooleddown and the raw oil gas can be warmed up. After cooling down, the thirdoil gas floats into the second condensation device 232, such as a platetype condenser, to be condensed as the finished oil, then, the finishedoil can be received by the receiving tank 240. Wherein, the ingredientof the finished oil can be a mixed or single liquor with high purity,such as Polyethylene, Polypropylene and/or Polystyrene with high purity.

As a result, the refining method for recycling waste plastics of thepresent invention uses the raw oil obtaining device and the rear enddevice to achieve the purpose of refining the waste plastics as therenewable oil with high purity and reduce the consumption of the fuelresource.

While the means of specific embodiments in present invention has beendescribed by reference drawings, numerous modifications and variationscould be made thereto by those skilled in the art without departing fromthe scope and spirit of the invention set forth in the claims. Themodifications and variations should in a range limited by thespecification of the present invention.

What is claimed is:
 1. A refining method for recycling waste plastics,at least comprising following steps: providing waste plastics in afeeding device; carrying the waste plastics to a rotary kiln of apyrolysis furnace, wherein the rotary kiln rotates the waste plastics;providing heat to the waste plastics in the rotary kiln by burning afuel via a burner, so that the waste plastics being cracked to produce aplastic gas, wherein the burner is assembled under the rotary kiln;introducing the plastic gas into a chloride-decomposing device havingammonia to remove chlorine of the plastic gas and produce a first oilgas and a mixed gas by reacting the waste plastics with the ammonia;condensing the first oil gas to produce a raw oil by a firstcondensation device; receiving the raw oil by a temporary storage;receiving the raw oil from the temporary storage by a still, wherein thestill warms up the raw oil to produce a second oil gas; introducing thesecond oil gas into a sieve plate tower, wherein the sieve plate towerhas a plurality of sieve plates arranged in a vertical direction orderlyto sieve the second oil gas, respectively, wherein a heavier oil gas ofthe second oil gas is transformed into an oil via the sieve plates andsent back to the still, and a lighter oil gas of the second oil gasfloats through the sieve plates to produce a third oil gas; condensingthe third oil gas to produce a finished oil by a second condensationdevice; and receiving the finished oil by a receiving tank.
 2. Therefining method for recycling waste plastics as defined in claim 1,wherein the step of carrying the waste plastics to a rotary kiln of apyrolysis furnace comprises the following steps: carrying the wasteplastics from the feeding device to a tundish by a bunker elevator; andextruding the waste plastics from the tundish to the rotary kiln by ascrew extruder.
 3. The refining method for recycling waste plastics asdefined in claim 1, wherein the mixed gas is carried to the burner forserving as the fuel by a pipe when the mixed gas is produced.
 4. Therefining method for recycling waste plastics as defined in claim 1,further comprising the following step: using a filtering tank and avacuum tank to accelerate the raw oil flowing to the temporary storage.5. The refining method for recycling waste plastics as defined in claim1, further comprising the following step: exchanging heat between thethird oil gas and the raw oil by a preheating device to cool down thethird oil gas and warm up the raw oil gas carried from the temporarystorage to the still when the third oil gas is produced.